EP0279456A2 - Verfahren zur Herstellung von Isobutylenpolymeren mit funktionalisierten Endgruppen - Google Patents

Verfahren zur Herstellung von Isobutylenpolymeren mit funktionalisierten Endgruppen Download PDF

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Publication number
EP0279456A2
EP0279456A2 EP88102462A EP88102462A EP0279456A2 EP 0279456 A2 EP0279456 A2 EP 0279456A2 EP 88102462 A EP88102462 A EP 88102462A EP 88102462 A EP88102462 A EP 88102462A EP 0279456 A2 EP0279456 A2 EP 0279456A2
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EP
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Prior art keywords
group
hydrocarbon
hydrogen atom
compound
general formula
Prior art date
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Application number
EP88102462A
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English (en)
French (fr)
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EP0279456B1 (de
EP0279456A3 (en
Inventor
Noda Kouji
Imanaka Masayoshi
Isayama Katsuhiko
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Kanegafuchi Chemical Industry Co Ltd
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Kanegafuchi Chemical Industry Co Ltd
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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F10/04—Monomers containing three or four carbon atoms
    • C08F10/08—Butenes
    • C08F10/10—Isobutene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F110/04—Monomers containing three or four carbon atoms
    • C08F110/08—Butenes
    • C08F110/10—Isobutene

Definitions

  • the present invention concerns a process for producing isobutylene polymers having a halogen atom or an RCOO- group, in which R is a hydrogen atom or monovalent organic group, at the terminal ends of the polymer chain. More specifically it relates to a process for producing isobutylene polymers in which a halogen atom or an RCOO- group is introduced in a high yield at the terminal ends of the polymer chain during cationic polymerization of a cationic polymerizable monomer containing isobutylene, in the presence of a specific initiator and chain transfer agent and a catalyst, and wherein the polymerization is conducted in the presence of a specific mixed solvent.
  • Polymers having functional end groups are well-­known and are useful as starting materials for adhesives, coating materials, sealants, etc.
  • Examples of such polymers include polyalkylene oxides having hydroxyl groups on both ends of the polymer chain, which are referred to as telechelic polymers, used to prepare poly­urethanes.
  • Isobutylene polymers having functional end groups can be produced by the INIFER process, in which isobutylene is cationically polymerized using a halogenated compound, such as 1,4-bis( ⁇ -chloroisopropyl) benzene (hereinafter referred to as p-DCC), as an initiator and chain transfer agent and a Lewis acid such as BCl3, as a catalyst. That process is described in U.S. Patent No. 4276394 specification of which is incorporated therein by reference.
  • p-DCC 1,4-bis( ⁇ -chloroisopropyl) benzene
  • Isobutylene polymers having chlorine atoms at both ends of the polymer chain obtained by the INIFER process can easily be converted by dehydrochlorination into a polymer having isopropenyl groups at both ends.
  • the polymer having isopropenyl groups can be readily converted by hydroboration to polymers having hydroxyl groups bonded to the primary carbon at each end of the polymer chain.
  • a primary object of the present invention is to provide a process for producing a polymer in which functional groups, such as halogen atoms, are introduced in a high yield to the ends of the polymer chain prepared using the INIFER process for the cationic polymerization of isobutylene.
  • polymers can be obtained in which functional groups, such as halogen atoms, are introduced in high yield at the terminal ends of the polymer chain.
  • the cationic polymerizable monomer containing isobutylene usable in the present invention is a monomer consisting solely of isobutylene or a mixture of isobuty­lene and a cationic polymerizable monomer copolymerizable with isobutylene.
  • mixtures containing not less than 50% (by weight, and hereinafter referred to as the same) of butylene in the total monomer is preferred.
  • the cationic polymerizable monomer copolymerizable with isobutylene preferably includes those compounds having ethylenically unsaturated bonds with 3 to 12 carbon atoms and can include, for example, olefins, with 3 to 12 carbon atoms conjugated dienes, vinyl ethers, aromatic vinyl compounds, vinyl silanes or allyl silanes. Among them, olefins or conjugated dienes with 3 to 12 carbon atoms are preferred.
  • cationic polymerizable monomer copolymerizable with isobutylene include, for example, propylene, 1-butene, 2-butene, 2-methyl-1-butene, 3-methyl-1-butene, pentene, 4-methyl-1-pentene, hexene, vinyl cyclohexane, butadiene, isoprene, cyclopentadiene, methyl vinyl ether, ethyl vinyl ether, isobutyl vinyl ether, styrene, ⁇ -methylstyrene, dimethylstyrene, monochlorostyrene, dichlorostyrene, ⁇ -pinene, indene, vinyltrichlorosilane, vinylmethyldichlorosilane, vinyldi­methylchlorosilane, vinyldimethylmethoxysilane, vinyltri­methylsilane, divinyldichlorosilane, divinylmethoxysilane, divinyldichlor
  • cationic polymer­izable monomers copolymerizable with isobutylene can be used alone or two or more of them be used together in combination with isobutylene.
  • the organic compound having the group represented by the general formula (I) is used as the initiator and as the chain transfer agent.
  • R1, R2 represent monovalent hydrocarbon groups in the general formula (I)
  • they are hydrocarbon groups with 1 to 20 carbon atoms.
  • Some of the hydrogen atoms in the hydrocarbon groups may partially be replaced by other substituents.
  • aliphatic hydrocarbon groups with 1 to 12 carbon atoms, such as methyl or ethyl group are preferred. If both R1, R2 are hydrogen atoms where R3 is an aliphatic hydrocarbon group, stable carbonium ions are not formed and polymerization does not progress smoothly.
  • R3 is preferably a hydrocarbon group with 1 to 40 carbon atoms. Some of the hydrogen atoms in the hydrocarbon group may be replaced by other substituents. R3 may be an aromatic hydrocarbon group or aliphatic hydrocarbon group. Examples of R3 can include: in which n is an integer of 1 to 5, m is an integer of 1 to 10 and n+1 is as defined above.
  • n is an integer of 1 to 5, and, most preferably, 1 or 2.
  • X represents a halogen atom or an RCOO- group.
  • the halogen atom can include, for example, fluorine, chlorine, bromine and iodine, with chlorine or bromine being preferred.
  • R is preferably a hydrogen atom or a hydrocarbon group with 1 to 6 carbon atoms and, particularly, an aliphatic hydrocarbon group.
  • the RCOO- group include, for example, CH3COO- and C2H5COO-.
  • Examples of the organic compound having the group represented by the general formula (I) includes those compounds represented by the general formula (II): AY l (II) where A represents a group having 1 to 4 aromatic rings, Y is a group represented by the general formula (III), attached to the aromatic ring: where R4 and R5 individually represent a hydrogen atom or a monovalent hydrocarbon group with 1 to 20 carbon atoms, X is a halogen atom or an RCOO- group and l represents an integer of 1 to 6; and a compound represented by the general formula (IV): BZ k (IV) wherein B represents a hydrocarbon group with 4 to 40 carbon atoms, Z represents a halogen atom or an RCOO- ­group (R has the same meaning as described above) attached to a tertiary carbon atom, and k represents an integer of 1 to 4; and oligomers having ⁇ -halostyrene units. These compounds may be used alone, or two or more of them may be used in combination.
  • the moiety A which is the group having 1 to 4 aromatic rings in the compound represented by the general formula (II) may be prepared by known procedures, for example, by condensation.
  • aromatic ring-containing groups include, for example, 1- ­to 6- valent phenyl, biphenyl, naphthalene, anthrathene, phenanthrene, pyrene, ph-(CH2) j -ph (where j is an integer from 1 to 10) etc.
  • These groups having aromatic rings may be substituted with aliphatic hydrocarbon groups with 1 to 20 hydrocarbons, or those groups having functional groups such as hydroxy, ether and vinyl.
  • the moiety Z in the compound represented by the general formula (IV) is a halogen atom or an RCOO- group attached to the tertiary carbon atom
  • the moiety B in the general formula (IV) is a hydrocarbon with 4 to 40 carbon atom and, preferably, aliphatic hydrocarbon group. If the number of carbon atoms is less than 4, a hydrogen atom or an RCOO- group does not remain bound to the tertiary carbon atom, and such compounds are not suitable for use.
  • the oligomer containing ⁇ -halostyrene units that can be used as the initiator and chain transfer agent can include, for example, an oligomer of ⁇ -chlorostyrene or an oligomer prepared by copolymerizing ⁇ -chlorostyrene and a monomer copolymerizable therewith.
  • a polymer having functionality on both terminal ends i.e., so-called telechelic polymer can be obtained.
  • Such polymer is extremely useful.
  • the initiator and chain transfer agent as described above can include, for example, organic compounds containing halogen atoms such as oligomers of ⁇ -chlorostyrene or organic compounds containing RCOO- groups.
  • halogen atom-containing organic compounds having -C(CH3)2Cl or -C(CH3)2Br capable of forming stable carbonium cations, for example, and those compounds in which chlorine atoms are replaced with bromine atoms in the above compounds such as Further, compounds containing CH3COO- group, such as are also preferred.
  • These compounds are the ingredient used as the initiator and as the chain transfer agent and the molecular weight of the polymer can be controlled by the amount used, usually about from 0.01 to 20% by weight and, preferably, from 0.1 to 10% by weight relative to the cationic polymerizable monomer containing isobutylene.
  • the Lewis acid used in the present invention is the ingredient used as the catalyst.
  • Typical examples of Lewis acids include those compounds represented by MX ⁇ n ⁇ (in which M represents a metal atom, X ⁇ represents a halogen atom and n ⁇ represents a positive integer).
  • MX ⁇ n ⁇ can include, for example, BCl3, AlCl3, SmCl4, TiCl4, VCl5, FeCl3 and BF3.
  • BCl3, AlCl3, BF3, etc. are preferred, with BCl3 being particularly preferred.
  • the amount of the Lewis acid is, preferably, from 0.1 to 10 moles and, more preferably, from 2 to 5 moles per mol of the initiator and the chain transfer agent utilized.
  • a hydrocarbon or a halogenated hydrocarbon containing an organonitro compound is used as the polymerization solvent.
  • halogenated hydrocarbons are preferred and, chlorinated hydrocarbons having one or two chlorine atoms are particularly preferred.
  • hydrocarbon and halogen­ated hydrocarbon can include, for example, pentane, hexane, CH3Cl, CH3CH2Cl, CH2Cl2, CH3CH2Cl, CH2ClCH2Cl, etc. They may be used alone or as a mixture and, further, may be used together with a small amount of other solvent.
  • organonitro compound contained in the hydrocarbon or halogenated hydrocarbon can include, for example, CH3NO2, CH3CH2NO2, 1-­nitropropane, 2-nitropropane, nitrobenzene, etc., and they may be used in admixture.
  • organonitro compounds those nitrohydrocarbons having one or two nitro groups are preferred.
  • the ratio of using one or more of the organonitro compound and one or more of the hydrocarbon or halogenated hydrocarbon as the main solvent is preferably from 0.1 to 100 parts by weight, more preferably, from 0.5 to 20 parts by weight of the organonitro compound based on 100 parts of one or more of the hydrocarbon or halogenated hydrocarbon.
  • the polymerization method may be batchwise charging solvent, monomer, initiator and chain transfer agent, catalyst, etc. successively into a vessel, or a continuous method of solvent, monomer, initiator and chain transfer agent, catalyst, etc. continuously charged into and taken out of a vessel.
  • the polymerization temperature is, preferably from -10 to -120°C and, more preferably from -20 to -80°C.
  • the polymerization time is preferably from 0.5 to 80 min and more preferably, from 1 to 30 min.
  • the monomer concentration upon polymerization is, preferably, about from 0.1 to 8M and, more preferably, about from 0.5 to 5M.
  • the organonitro compounds may be added directly to the main solvent, or added to the solution of the initiator and chain transfer agent or added to the catalyst solution. Further, a catalyst solution prepared from the organonitro compound and the catalyst may be added, and these methods can be employed in combination.
  • the polymerization is preferably stopped by the addition of alcohols such as methanol.
  • a stirring blade, a three-way stopcock and a vacuum line were attached to a 1 liter autoclave made of pressure-proof glass and, while evacuating through the vacuum line, the polymerization vessel was dried by heating at 100°C for one hour and, after cooling to the room temperature, the pressure was returned to the normal pressure by opening the three-way stopcock.
  • the polymerization vessel was immersed in a dry ice-acetone bath -70°C and cooled for one hour while stirring its contents. After cooling, the pressure of the inside was reduced via the vacuum line, the needle valve was opened and isobutylene was introduced from the liquefied gas sampling tube made of pressure-proof glass into the polymerization vessel. Then, the pressure was returned to normal pressure by introducing nitrogen from one end of the three-way stopcock and the contents of the polymerization vessel were cooled to -60°C by continuing the cooling for one hour under stirring.
  • boron trichloride solution (containing 20 mmol of boron trichloride) was added from the three-way stopcock by an injection cylinder to start the polymerization and, after the elapse of 30 min, methanol previously cooled to lower than -40°C was added to stop the polymerization.
  • the temperature of the polymerization vessel was returned to the room temperature and the reaction mixture was taken out into a eggplant-shaped flask to remove unreacted isobutylene, methylene chloride, nitromethane and methanol by distillation. After dissolving the residual polymer in 400 ml of n-hexane, the solution was repeatedly washed with water till it became neutral. Then, the n-hexane solution was concentrated to 80 ml and the concentrated solution poured into a one liter of acetone to settle and separate the polymer.
  • the thus obtained polymer was again dissolved into 400 ml of n-hexane, dried over anhydrous magnesium sulfate, and filtered to removed n-hexane under a reduced pressure to obtain the purified isobutylene polymer.
  • the yield was calculated from the amount of the resultant polymer produced, n and w/ n were determined by GPC, and the end structure was determined by measuring and comparing the intensity of proton resonance signals belonging to each of the structures by the H1-NMR (300 MHz) method. The results are shown in Table 1.
  • Polymer was produced in the same manner and evaluated as in Example 5 excepting for not using the organonitro compound. The results are shown in Table 2.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Polymerisation Methods In General (AREA)
  • Polymerization Catalysts (AREA)
EP88102462A 1987-02-20 1988-02-19 Verfahren zur Herstellung von Isobutylenpolymeren mit funktionalisierten Endgruppen Expired - Lifetime EP0279456B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP38778/87 1987-02-20
JP62038778A JPH0651752B2 (ja) 1987-02-20 1987-02-20 官能性末端を有するイソブチレン系ポリマ−の製造法

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EP0279456A2 true EP0279456A2 (de) 1988-08-24
EP0279456A3 EP0279456A3 (en) 1990-04-04
EP0279456B1 EP0279456B1 (de) 1995-05-03

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US (1) US4870144A (de)
EP (1) EP0279456B1 (de)
JP (1) JPH0651752B2 (de)
DE (1) DE3853691T2 (de)

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Publication number Priority date Publication date Assignee Title
EP0435116A2 (de) * 1989-12-23 1991-07-03 BASF Aktiengesellschaft Verfahren zur Reinigung von Polymerisaten des Isobutens
EP0556965A1 (de) * 1992-02-19 1993-08-25 BP Chemicals Limited Poly(iso)butenen
GB2269180A (en) * 1992-07-14 1994-02-02 Air Prod & Chem Process for the synthesis of oligomeric vinylamides and vinylamines
EP0807641A2 (de) * 1996-05-13 1997-11-19 Basf Aktiengesellschaft Verfahren zur Herstellung von mittelmolekularem, hochreaktivem Polyisobuten
WO2001036498A1 (en) * 1999-11-15 2001-05-25 Exxon Chemical Patents Inc. Production of isobutylene copolymers
EP1122267A1 (de) * 2000-01-31 2001-08-08 Bayer Ag Hochmolekulare gelfreie Isobutencopolymere mit hohen Doppelbindungsgehalten
WO2002018460A1 (de) * 2000-08-28 2002-03-07 Bayer Aktiengesellschaft Verfahren zur herstellung von isoolefincopolymeren
WO2002048215A2 (de) * 2000-12-12 2002-06-20 Basf Aktiengesellschaft Verfahren zur herstellung von polyisobutenen
WO2002050141A1 (en) * 2000-12-20 2002-06-27 Exxonmobil Chemical Patents Inc. Process for polymerizing cationically polymerizable monomers
US6525149B1 (en) 1999-09-16 2003-02-25 Texas Petrochemicals, Lp Process for preparing polyolefin products
US6562913B1 (en) 1999-09-16 2003-05-13 Texas Petrochemicals Lp Process for producing high vinylidene polyisobutylene
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US6777506B1 (en) 2003-05-09 2004-08-17 Texas Petrochemicals, Lp Apparatus for preparing polyolefin products and methodology for using the same
US6884858B2 (en) 1999-10-19 2005-04-26 Texas Petrochemicals Lp Process for preparing polyolefin products
US6992152B2 (en) 1999-10-19 2006-01-31 Texas Petrochemicals Lp Apparatus and method for controlling olefin polymerization process
US7037999B2 (en) 2001-03-28 2006-05-02 Texas Petrochemicals Lp Mid-range vinylidene content polyisobutylene polymer product and process for producing the same
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US7956138B2 (en) 2007-05-16 2011-06-07 Exxonmobil Chemical Patents Inc. Catalyst system for olefin polymerization and polymers produced therefrom
EP2502742A2 (de) 2005-10-27 2012-09-26 ExxonMobil Chemical Patents Inc. Konstruktion mit einer Bindeschicht für Luftreifen
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Cited By (44)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0435116A3 (en) * 1989-12-23 1992-02-26 Basf Aktiengesellschaft Process for the purification of polymers of isobutylene
EP0435116A2 (de) * 1989-12-23 1991-07-03 BASF Aktiengesellschaft Verfahren zur Reinigung von Polymerisaten des Isobutens
EP0556965A1 (de) * 1992-02-19 1993-08-25 BP Chemicals Limited Poly(iso)butenen
GB2269180A (en) * 1992-07-14 1994-02-02 Air Prod & Chem Process for the synthesis of oligomeric vinylamides and vinylamines
GB2269180B (en) * 1992-07-14 1996-11-20 Air Prod & Chem Process for the synthesis of oligomeric vinylamides and vinylamines
EP0807641A2 (de) * 1996-05-13 1997-11-19 Basf Aktiengesellschaft Verfahren zur Herstellung von mittelmolekularem, hochreaktivem Polyisobuten
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EP0279456B1 (de) 1995-05-03
US4870144A (en) 1989-09-26
EP0279456A3 (en) 1990-04-04
JPH0651752B2 (ja) 1994-07-06
JPS63205304A (ja) 1988-08-24
DE3853691D1 (de) 1995-06-08

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